Patent GB-919028-A (GB)
Title: Improvements in method and apparatus for treating gaseous and non-gaseous matter forremoving contaminants from the gaseous matter
IPC: F27B7/20
Filed: 1959-04-09
Abstract: 919,028. Filtering gases. FULLER CO. April 9, 1959 [May 6, 1958], No. 12008/59. Class 8(2). [Also in Group XII]. A method of purifying gases includes the steps of passing a plurality of streams of non- gaseous matter downwardly in troughs through a moving gaseous body containing pollutants, causing the gases of the body to pass in a vertical direction completely around the troughs with resultant repeated changing of the direction of flow of the gases as they pass about the troughs to agitate pollutants contained in the gases, maintaining direct contact between the gaseous body and at least a portion of the matter of each of the streams with resultant deposition of pollutant matter into the streams from the gaseous body, and separating the streams and the gaseous body, The non- gaseous matter passing along the troughs may be a liquid such as water or it may consist of solid particles. The method is particularly applicable to the purification of gases discharged from a cement kiln, the gases being simultaneously utilized to preheat the cement raw materials. Thus, in this instance, the hot gases from the cement kiln may first pass to a chamber containing troughs, down which the cement raw materials pass to the kiln. In this chamber, the cement raw materials are preheated and the major proportion of pollutants, such as dust particles, is removed from the gases. Then the gases may proceed to a second chamber containing troughs, down which water runs. In the second chamber, the remainder of the pollutants, especially fine dust particles and alkali vapours, is removed from the gases. In another application of the method, the gases are cool and the solid material passed down the troughs is hot cement clinker. In Fig. 2, the apparatus employed is divided into two sub-chambers 7 (see also Fig. 3) and 8 (see also Fig. 4) subchamber 7 having a series of troughs 14, 14a down which cement raw materials flow and sub-chamber 8 having a series of troughs 62 down which water flows. The baffle wall 9 between sub-chambers 7 and 8 terminates short of the roof 6 of the apparatus to allow passage of gas from one sub-chamber to the other. Hot gases from the cement kiln enter sub-chamber 7 at 2 and, having reached the top of this subchamber, pass down sub-chamber 8 to gas outlet 10, proceeding thence via fan 12 to exhaust stack 13. Cement raw materials from supply hopper 22 are pumped by pump 21, via conduit 20, to distributer 17 and then flow down troughs 14a to collecting hopper 35. The cement raw materials are then pumped by pump 37 via conduit 38, to distributer 24 and then flow down troughs 14 to collecting hopper 42. Finally, the cement raw materials pass to the kiln along pipe 44. Water from the main via pipe 74, or from a settling pond via pipe 69, is pumped by pump 68, through pipe 70 and distributing pipes 73 into trays 61. From these, the water runs through spouts 76 into troughs 62, which carry the water along their slope to the next lower tray on the opposite wall of sub-chamber 8. Finally the water passes down drains 64 into collecting pan 65 and is delivered by conveyer 66 to the settling pond 67. Sludge may be removed from the settling pond, dewatered and mixed in mixer M with cement raw materials passing down the overflow line 39 from distributer 24. The sludge thus becomes blended with the raw materials pumped by pump 21 to distributer 17. According to a modification, water is fed to the troughs down which the cement raw materials are passing in order to cause the materials to form nodules and the troughs are vibrated to assist the downward flow of the materials. Specifications 919,029 and 919,030 are referred to.